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RU2003111161A - METHOD FOR PARTIAL OXIDATION OF METHANE USING DENSE CERAMIC MEMBRANE WITH SELECTIVE OXYGEN PERMEABILITY - Google Patents

METHOD FOR PARTIAL OXIDATION OF METHANE USING DENSE CERAMIC MEMBRANE WITH SELECTIVE OXYGEN PERMEABILITY Download PDF

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Publication number
RU2003111161A
RU2003111161A RU2003111161/15A RU2003111161A RU2003111161A RU 2003111161 A RU2003111161 A RU 2003111161A RU 2003111161/15 A RU2003111161/15 A RU 2003111161/15A RU 2003111161 A RU2003111161 A RU 2003111161A RU 2003111161 A RU2003111161 A RU 2003111161A
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Russia
Prior art keywords
methane
membrane
partial oxidation
catalyst
partial
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RU2003111161/15A
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Russian (ru)
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Хидеки КУРИМУРА (JP)
Хидеки КУРИМУРА
Соити КАГАНОИ (JP)
Соити КАГАНОИ
Ехеи СУЗУКИ (JP)
Ехеи СУЗУКИ
Original Assignee
Тейкокуойл Ко., Лтд. (Jp)
Тейкокуойл Ко., Лтд.
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Publication of RU2003111161A publication Critical patent/RU2003111161A/en

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    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/386—Catalytic partial combustion
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/8933—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/8946—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with alkali or alkaline earth metals
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • B01J35/58—Fabrics or filaments
    • B01J35/59—Membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/024—Multiple impregnation or coating
    • B01J37/0248—Coatings comprising impregnated particles
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02—Preparation of oxygen
    • C01B13/0229—Purification or separation processes
    • C01B13/0248—Physical processing only
    • C01B13/0251—Physical processing only by making use of membranes
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
    • C01B2203/0261—Processes for making hydrogen or synthesis gas containing a partial oxidation step containing a catalytic partial oxidation step [CPO]
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/10—Catalysts for performing the hydrogen forming reactions
    • C01B2203/1041—Composition of the catalyst
    • C01B2203/1047—Group VIII metal catalysts
    • C01B2203/1052—Nickel or cobalt catalysts
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/10—Catalysts for performing the hydrogen forming reactions
    • C01B2203/1041—Composition of the catalyst
    • C01B2203/1047—Group VIII metal catalysts
    • C01B2203/1064—Platinum group metal catalysts
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1205—Composition of the feed
    • C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
    • C01B2203/1235—Hydrocarbons
    • C01B2203/1241—Natural gas or methane
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/12—Feeding the process for making hydrogen or synthesis gas
    • C01B2203/1258—Pre-treatment of the feed
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2210/00—Purification or separation of specific gases
    • C01B2210/0043—Impurity removed
    • C01B2210/0046—Nitrogen
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • General Health & Medical Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Catalysts (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Claims (6)

1. Способ частичного окисления метана с использованием мембранного реактора, в котором воздух приводят в контакт с одной стороны плотной керамической мембраны с селективной проницаемостью для кислорода, и газовое сырье, которое содержит метан в качестве основного компонента, подают в контакт с другой стороны мембраны таким образом, чтобы провести частичное окисление метана с помощью кислорода, который селективно проходит через керамическую мембрану со стороны воздуха на сторону метана, отличающийся тем, что катализатор частичного окисления метана размещают при двухмерной схеме расположения контакта с указанной мембраной в верхней части сырьевого газового потока и катализатор частичного окисления метана размещают при трехмерной схеме расположения контакта с указанной мембраной в нижней части потока.1. The method of partial oxidation of methane using a membrane reactor, in which air is brought into contact on one side of a dense ceramic membrane with selective permeability to oxygen, and a gas feed that contains methane as the main component is fed into contact on the other side of the membrane in this way in order to conduct partial oxidation of methane with oxygen, which selectively passes through a ceramic membrane from the air side to the methane side, characterized in that the partial oxide catalyst methane lines are placed in a two-dimensional contact arrangement with said membrane in the upper part of the feed gas stream and a partial methane oxidation catalyst is placed in a three-dimensional contact arrangement with said membrane in the lower part of the stream. 2. Способ частичного окисления метана с использованием мембранного реактора по п.1, в котором указанное газовое сырье представляет собой природный газ, газ угольного месторождения, газ от пиролиза угля и/или газ коксовой печи, который содержит метан.2. The method of partial oxidation of methane using the membrane reactor according to claim 1, wherein said gas feed is natural gas, coal gas, gas from coal pyrolysis and / or coke oven gas that contains methane. 3. Способ частичного окисления метана с использованием мембранного реактора по п.1, где в качестве средства размещения катализатора частичного окисления метана на основе Ni или благородного металла, такого как Ru, на керамической мембране при двухмерной схеме расположения контакта, используют суспензию, полученную из тонкодисперсного порошка катализатора, включающего носитель, который смешивают с органическим растворителем, наносят на керамическую мембрану, которую затем обжигают для спекания катализатора.3. The method of partial oxidation of methane using the membrane reactor according to claim 1, where as a means of placing a catalyst for partial oxidation of methane based on Ni or a noble metal such as Ru on a ceramic membrane with a two-dimensional contact arrangement, a suspension obtained from a finely dispersed one is used catalyst powder, including a carrier, which is mixed with an organic solvent, is applied to a ceramic membrane, which is then calcined to sinter the catalyst. 4. Способ частичного окисления метана с использованием мембранного реактора по п.1, где в качестве средства размещения катализатора частичного окисления метана на основе Ni или благородного металла, такого как Ru, на керамической мембране при трехмерной схеме расположения контакта, пространство подвода потока в реакторе заполняют порошком катализатора, включающим носитель, в частичном контакте с керамической мембраной.4. The method of partial oxidation of methane using the membrane reactor according to claim 1, where, as a means of placing the catalyst for partial oxidation of methane based on Ni or a noble metal such as Ru, on a ceramic membrane with a three-dimensional contact arrangement, the space for supplying a stream in the reactor is filled catalyst powder, including the carrier, in partial contact with a ceramic membrane. 5. Способ частичного окисления метана по п.3 или 4, где используемый катализатор частичного окисления металла на основе Ni имеет состав, представленный Nix/CaySr1-yTiO3 (х=от 0,1 до 0,3, у=0,8 или 0,0) или Nix/BaTiO3 (х=от 0,1 до 0,3), с рутением, платиной или родием, нанесенными на него в соотношении от 0,1 до 1000 млн-1 по весу указанного катализатора.5. The method of partial oxidation of methane according to claim 3 or 4, wherein the Ni-based partial metal oxidation catalyst used has the composition represented by Ni x / Ca y Sr 1-y TiO 3 (x = 0.1 to 0.3, y = 0.8 or 0.0) or Ni x / BaTiO 3 (x = 0.1 to 0.3), with ruthenium, platinum or rhodium deposited on it in a ratio of from 0.1 to 1000 million by -1 the weight of the specified catalyst. 6. Способ частичного окисления метана с использованием мембранного реактора по п.1, где пар смешивают в потоке газового сырья, которое содержит метан в качестве основного компонента, при соотношении от 0,25 до 0,5 пара к количеству содержащегося углерода.6. The method of partial oxidation of methane using a membrane reactor according to claim 1, where the vapor is mixed in a stream of gas raw materials that contains methane as the main component, in a ratio of 0.25 to 0.5 steam to the amount of carbon contained.
RU2003111161/15A 2000-09-20 2001-09-17 METHOD FOR PARTIAL OXIDATION OF METHANE USING DENSE CERAMIC MEMBRANE WITH SELECTIVE OXYGEN PERMEABILITY RU2003111161A (en)

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JP2000-284647 2000-09-20
JP2000284647 2000-09-20

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US (1) US7105147B2 (en)
EP (1) EP1333009A4 (en)
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AU (1) AU2001286258A1 (en)
CA (1) CA2422567A1 (en)
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EP1333009A1 (en) 2003-08-06
US20040101472A1 (en) 2004-05-27
ZA200303049B (en) 2004-04-19
JPWO2002024571A1 (en) 2004-01-29
JP4953546B2 (en) 2012-06-13
CN1461282A (en) 2003-12-10
NO20031264L (en) 2003-05-19
NO20031264D0 (en) 2003-03-19
AU2001286258A1 (en) 2002-04-02
WO2002024571A1 (en) 2002-03-28
US7105147B2 (en) 2006-09-12
CA2422567A1 (en) 2003-03-18
EP1333009A4 (en) 2004-08-04

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